Two component powder coating system and method for coating wood therewith

ABSTRACT

Wood is electrostatically coated with a thermosetting powder coating system in which a mixture of a self-curing epoxy resin and a catalyst therefore is extruded and a low temperature curing agent are both pulverized and the powders are blended with conventional additives to make a coating powder which is deposited on a wooden substrate and heated to cure. The mixture of resin and catalyst does not cure within the extruder but it is made to cure at low temperatures by the separate addition of the curing agent. A small amount of the low temperature curing agent, insufficient to cause substantial curing during extrusion may be used in place of the catalyst.

This is a divisional of application Ser. No. 08/810,745 filed on Mar. 4, 1997:, U.S. Pat. No. 5,714,206 which is a C-I-P of Ser. No. 08/729,608 filed Oct. 11, 1996, abandoned, which is a C-I-P of Ser. No. 08/643,694 filed May 6, 1996, abandoned.

BACKGROUND OF THE INVENTION

This invention relates to a two-component powder coating system by which the curing of a coating occurs at a significantly faster rate and/or at a significantly lower temperature and produces an exceptionally smooth surface. This invention also relates to thermally stable powder coating whereby white coatings do not yellow during thermal curing. This invention also relates to the electrostatic coating of metal and, in particular, to the triboelectric coating of wood with a coating powder and low temperature curing of that coating having a pleasing smoothness.

Traditionally, coating powders have been made by the extrusion of a mixture of resins and curing agents to obtain a homogeneous mixture and then grinding the extrudate and screening the comminuted product to obtain the desired particle sizes and particle size distribution. The powder is then electrostatically sprayed onto a substrate, traditionally a metal substrate, and cured at temperatures much higher than 200° F. The curing of powder coatings on heat sensitive materials such as wood, plastic, and the like has been limited by the fact that the extrusion of a mixture of a resin and a low temperature curing agent, i.e., one that is active at 200° F. or less, would cause the coating powder to gel in the extruder because the extrusion typically generates enough heat to raise the temperature to 200° F. or higher. It has been thought throughout the art that the curing agent must be mixed with the resin by extrusion to obtain a uniform cure and film appearance. It has also been commonly accepted that a low gloss film must be cured at a high temperature, e.g., about 300° F. or higher.

The powder coating of wood has been much talked about in the literature but very little has been said as to how it may be accomplished. As Douglas S. Richart said in his article published in the April, 1996 issue of POWDER COATINGS, the coating of wood with a low temperature cure powder is next to impossible because the coating must be cured at a temperature below 200° F. and the resin must have a flow temperature of about 10 to 20 degrees lower than that. Such a resin tends to block during storage at normal temperatures. Richart goes on to say that the curing agent must be sufficiently reactive that the powder will cure in a reasonable time at such low temperatures. But that leads to a possible thermosetting of the resin in the extruder. He speaks of electrostatically spraying a powder having a blocked isocyanate onto wood, heating the coating in infra-red and other type ovens to form a smooth coating and curing the smooth coating with ultra-violet radiation.

In its technical bulletins, Boise Cascade shows the use of hand-held electrostatic spray guns in coating its electrically conducting particleboard.

In this invention, the epoxy resin is first extruded with a small amount of catalyst or with a low level of a low temperature curing agent and then ground and classified in the usual manner. Additional amounts of the low temperature curing agent in powder form are then blended with the powdered extrudate raise the level of curing agent while avoiding the pre-gelation problem. Surprisingly, the time required to obtain a smooth cured film is lowered significantly. It was surprising, also, that a low gloss film was achieved at cure temperatures much lower than 300° F.

SUMMARY OF THE INVENTION

It is an object of this invention, therefore, to provide a coating powder for heat sensitive substrates.

It is a related object of this invention to provide a method for coating wood without the problems associated with volatile organic solvents.

It is another object of this invention to provide a low temperature process for producing a smooth, low gloss coating on wood.

These and other objects of the invention which will become apparent from the following description are achieved by a thermosetting powder coating system in which the thermosetting of an extruded mixture of a self-curing epoxy resin and (A) a catalyst or (B) an amount of a low temperature curing agent insufficient to cause substantial curing of the resin during extrusion is facilitated by the separate addition of a low temperature curing agent; said extruded mixture and said separately added low temperature curing agent both being in powder form and being blended to form a coating powder.

DETAILED DESCRIPTION OF THE INVENTION

The curing system of this invention may be used in coating glass, ceramics, and graphite-filled composites as well as metallic substrates such as steel and aluminum but its particular utility in the coating of heat sensitive subsrates such as plastics, paper, cardboard and woods makes it highly appealing as a commercially viable alternative to the liquid coatings that have been almost universally used in the past. For the purposes of this invention, wood is defined as any lignocellulosic material whether it comes from trees or other plants and whether it be in its natural forms, shaped in a saw mill, separated into sheets and made into plywood, or chipped and made into particleboard, or its fibers have been separated, felted, and compressed. It is exemplified by lumber, panels, molding, siding, oriented strand board, hardboard, medium density fiberboard, and the like. The particle board may be standard or treated to enhance its electrical conductivity. Wood having a moisture content of from 3 to 10% by weight is suitable for the purposes of this invention. A porous particleboard, pre-coated with a conductive liquid coating composition and cured, may also serve as a substrate for the coating powder of this invention. For example, a smooth 2-3 mil thick powder coating is achieved on a 0.5 to 1 mil thick UV or thermally cured pre-coat. Without the precoat, a smooth powder coating must be about 9 mils thick.

A particularly favored embodiment of the system is one in which competing reactions are taking place simultaneously, said reactions being:

(A) a catalyzed self-curing of a portion of an epoxy resin present in an extruded mixture of the resin and a catalyst, and

(B) a crosslinking reaction between another portion of the extruded resin and a low temperature curing agent.

Epoxy resins which are useful in the practice of this invention are exemplified by, but not limited to, those produced by the reaction of epichlorohydrin and a bisphenol, e.g., bisphenol A. Preferred epoxy resins include those sold under the trademarks ARALDITE GT-7072, 7004, 3032, 6062, and 7220, and EPON 1007F, 1009F, and 1004, all of which are 4,4'-isopropylidenediphenol-epichlorohydrin resins.

The epoxy resin is self-curing, i.e., it reacts via homopolymerization during curing of the powder coating. Generally, a catalyst is required to cause the reaction to progress at a commercially acceptable rate. A preferred catalyst for this invention is an epoxy adduct of an imidazole having the general formula: ##STR1## wherein R¹, R², R³, and R⁴ are independently hydrogen or any substituent which is not reactive with the epoxy resin. Examples of suitable imidazoles include imidazole, 2-methyl imidazole, and 2-phenyl imidazole. Suitable adducts of such imidazoles with a bisphenol A epoxy resin are available commercially from Shell Chemical Company under its trademark EPON, e.g., EPON P-101, and also from Ciba-Geigy Corporation under its designation XU HT 261. For the purposes of this invention, the term imidazole is used herein to mean both the substituted and unsubstituted imidazoles. Although applicants are not bound to any theory, it is believed that an imidazole adducts to epoxy resins by an opening of the epoxy ring that results in the epoxy oxygen bonding to the C═N bond of the imidazole ring. The adducted imidazole acts as a catalyst, moving from one epoxy group to another as it facilitates epoxy ring opening and cure reactions. Imidazoles, in themselves, tend to be insoluble in epoxy resins. Thus, the purpose for adducting them to an epoxy resin is to make them compatible with the epoxy system. As a catalyst, the imidazole adduct is used in the systems, methods, and powders of this invention at a level of from about 0.1 to about 8 parts per hundred parts of the extruded resin (phr), preferably at about 2 phr. For enhanced color stability, the 2-phenyl imidazole may be used as the catalyst for curing the epoxy resin with or without the low temperature curing agent. The 2-phenyl imidazole, which is available from the SWK Chemical Co., may be used as such at accordingly lower levels.

The imidazoles, as adducts or non-adducts, may also used at higher levels as a separately added curing agent to the extruded mixture of the resin and catalyst. When this is done, the amount of imidazole adduct is controlled so that the total amount is no more than about 12 phr.

Otherwise, the low temperature curing agent may be selected from among the many that are commercially available but an epoxy adduct of an aliphatic polyamine having a primary amino group is preferable. A suitable curing agent of that type is available from Ciba Ceigy as its PF LMB 5218 hardener. A similar product is sold under the trademark ANCAMINE 2337 XS by Air Products & Chemicals. An epoxy adduct of an aliphatic polyamine having a secondary amino group available under the trademark ANCAMINE 2014 AS is preferred for white and light colored coatings. The amount of low temperature curing agent that may be added separately as component (B) to the pulverized extrudate of resin and catalyst is from about 2 to about 40 phr and the preferred amount is from about 30 to about 35 phr. The ratio of the low temperature curing agent to the catalyst in the extrudate is from about 1:3 to about 400:1 but preferably from about 2:1 to about 15:1.

The coating powder may also contain a flow control agent in the range of from about 0.5 to about 2.0 phr. Examples of the flow control agents include the MODAFLOW poly(alkylacrylate) products and the SURFYNOL acetylenic diols; they may be used singly or in combination. Anti-oxidants may also be used at a concentration of from about 0.5 to about 2.0 phr to prevent the discoloration of the coatings even at the relatively low curing temperatures suitable for the purposes of this invention. Examples of the anti-oxidants that are useful in this invention include sodium hypophosphite, tris-(2,4-di-t-butyl phenyl) phosphite (sold under the trademark IRGAFOS 168), and calcium bis( monoethyl(3,5-di-t-butyl-4-hydroxybenzyl)phosphonate! (sold under the trademark IRGANOX 1425). Mixtures of anti-oxidants may be used.

Pigments, optical brighteners, fillers such as calcium carbonate and bentonite clays, texturizing agents such as particulate rubber, and other conventional additives may also be present. A particularly desirable textured finish may be obtained by the addition of from about 14 to about 20 phr of the rubber to the coating composition along with calcium carbonate at a rubber to carbonate ratio of from about 0.7:1 to about 1.5:1 by weight. Titanium oxide, in an amount of from about 5 to about 50 phr or more, is an example of a pigment that may be used. An optical brightener, exemplified by 2,2'-(2,5-thiophenediyl)bis 5-t-butylbenzoxazole, sold under the trademark UVITEX OB, may be present at from about 0.1 to about 0.5 phr.

For the purposes of this invention, the term resin includes the resin per se and the crosslinking agent whether it is in the extrudate or it is added separately but it does not include the catalyst.

The coating powder of this invention may be applied by any of the conventional powder coating methods but the application of the powder by triboelectric guns is preferred in particular situations such as when the wooden substrate is profiled. The grooves and ridges present a particular problem for electrostatic coating processes because of the Faraday effect. Because the electrical field generated by friction as the powder flows along the TEFLON plastic surfaces inside the gun is relatively small in comparison with the field in a corona-discharge cloud, the powder particles may be deposited more efficiently into Faraday cage areas with triboelectric guns. Wooden cabinet doors are examples of a profiled wooden substrate as are the doorskins represented by the drawings in U.S. Pat. No. 5,489,460, which is incorporated herein by reference to further illustrate the type of wooden panels that are particularly susceptible to powder coating by the method of this invention. The grooves and sharp edges of such panels are covered very well on a flat line coating apparatus with nozzles arrayed to direct a portion of the powder against them.

Such panels as well as flat-surfaced panels such as those used to make ping-pong tables are particularly well coated by triboelectric guns on a flat line conveyor having electrically conductive bands around the circumference of the conveyor belt. Apparatus for such coating is disclosed in a series of patents assigned to the Nordson Corporation. These are U.S. Pat. Nos. 4,498,913; 4,590,884; 4,723,505; 4,871,380; 4,910,047; and 5,018,909; all of which are incorporated herein by reference. A suitable flat line powder coating apparatus comprises such a conveyor extending through a powder coating booth, wherein a wooden article supported and moved by the conveyor belt is coated triboelectrically by a plurality of guns situated adjacent one another and in one or more tiers. The powder is forced into the guns under about 40 psi pressure and air at about 20 psi is passed into the powder conduits just before the powder passes into the nozzles. The article bearing the powder is then conveyed through a curing oven having several heating zones, some of which are heated by IR lamps, others by heat convection, and still others by a combination of those two. The coating and curing line speeds may be the same or different depending on the the length of the curing oven. The line speed through the powder application booth may be from about 5 to about 150 feet per minute but it is preferably from about 20 to about 100 feet per minute. The line speed through the curing oven, on the other hand, may be from about 5 to about 20 feet per minute, depending on the oven temperature and the particular coating powder used. The curing temperature may range from about 180° up to but not including the decomposition temperature of the powder. It is preferred to maintain the cure temperature within the range of from about 190° to about 290° F. and still more preferred to keep the cure temperature at from about 250 to about 290° F. When a crystalline epoxy resin is used, a cure temperature of about 180° F. is particularly suitable. It is preferred that the coating and curing line speeds be adjusted to the oven length so that they are balanced.

Preheating of the panel before the coating step is preferred in some instances, e.g., to help the powder reach its flow temperature in the first zone of the oven and it also minimizes outgassing during cure. The oven may have several heating zones of the IR and convection types and also a combination of the two. The TRIAB Speedoven sold by Thermal Innovations Corporation is suitable for the purposes of this invention. A wooden panel bearing a coating powder of this invention may be cured in a gas-fired IR oven available from Thermal Innovations Corporation by pre-heating the panel in the oven at an emitter temperature of about 1800° F. for from about 4 to about 10 seconds and post-heating at the same emitter temperature for from about 6 to about 10 seconds. When a medium density fiberboard (at about 40° F.), was pre-heated and post-heated at 1800° F. for about 6 seconds and 6.5 seconds, respectively, the surface of the panel next to the IR emitter was about 310° F. after the pre-heating and the post-heating, alike. The surface opposite the IR emitter was about 50° F. as it left the oven. Such relatively cool panels may be stacked atop one another as they come out of the oven. A higher emitter temperature may be used for proportionally shorter times.

The film thickness of the cured coating is at least about 1 mil and it may be as much as about 8 mils or even higher if there is a practical need for such. Film thicknesses of from about 4 to about 6 mils are achieved regularly by the method of this invention, even at coating line speeds of about 100 feet per minute.

The invention is more specifically described in the following working examples wherein parts are by weight unless otherwise stated.

EXAMPLES 1-4 and CONTROL

Coating powders were made as described above from the following components:

    __________________________________________________________________________     COMPONENTS                  (A)    (A*)          (B)                  RESIN WITH                         RESIN (A**)   PIGMENT                                             (B*)                  CATALYST &                         PIGMENT                               CRYSTALLINE                                       & CURING                  PIGMENT                         ONLY  EPOXY   AGENT CATALYST     __________________________________________________________________________     Crystalline Epoxy RSS 1407                  --     --    50      --    --     Epoxy Resin GT-7072                  100    100   50      --    --     Imidazole Adduct P-101                  2      --    --      --    100     Acrylate Flow Acid                  1.4    1.4   1.4     1.4   --     Benzoin      .8     .8    --      .8    --     Pigments     .079   .079  --      .079  --     TiO.sub.2 R-902                  60     60    --      60    --     Amine Adduct LMB-5218                  --     --    --      100   --     UVI 6974 Catalyst*                  --     --    2       --    --     __________________________________________________________________________      *substantially nonfunctional under these conditons

                  TABLE 1     ______________________________________                                      Control     EXAMPLE     1     2     3    4   Conventional Extrusion     ______________________________________     Component A 70    --    100  --  100     Component A*                 --    70    --   --  --     A**         --    --    --   70  --     Component B 30    30    --   --  --     Component B*                 --    --      3  --  --     LMB 5218 adduct                 --    --    --   30  --     ______________________________________

The powders of these examples were electrostatically coated on steel panels and cured at 225° F. for 10 minutes to obtain 1.8-2.2 mil thick films. As shown in Table 2, the superior solvent resistance of Examples 1 and 3 demonstrate that faster cure is achieved using this technology. Neither the conventionally extruded material (Control) nor the blend with no catalyst in Component A (Example 2) achieved full cure.

                  TABLE 2     ______________________________________     EXAMPLE 1        2        3      4      Control     ______________________________________     MEK     Moderate Rubs     No     Moderate                                             Rubs     Resistance             Rub Off  Through  Effect Rub Off                                             Through     (50 Double     Rubs)     Impact  140 in-lbs                      80 in-lbs                               60 in-lbs                                      100 in-lbs                                             0 in-lbs     Resistance     (Direct)     60° Gloss             40       15       78     32     80     Orange Peel             Slight   Moderate Slight Very   Slight                                      Slight     ______________________________________

                                      TABLE 3     __________________________________________________________________________     Examples 5-8     Ex.        Line Speed                      Preheat Setting                                Line Speed in                                       Actual Temp.       Mek Rate                                                                Thick-     # Powder           Substrate                of Coating                      IR or Conv.                                Curing Oven                                       Exiting IR                                              Appearance  Double                                                                ness     __________________________________________________________________________     5 Ex. 1           MDF  30 ft/min                      None      5 ft/min                                       290° F.                                              No outgassing/slight                                                          #4llow                                                                4+                                              Low Gloss/Smooth     6 Ex. 1           MDF  30 ft/min                      None      6 ft/min                                       240° F.                                              Slight Outgassing/white                                                          #3    4+                                              Higher Gloss/Slight OP     7 Ex. 1           MDF  30 ft/min                      None      5 ft/min                                       260° F.                                              No outgassing/slight                                                          #4llow                                                                4+                                              Low Gloss/Smooth     8 Ex. 1           MDF  30 ft/min                      Yes       10 ft/min                                       250-280° F.                                              No outgassing/slight                                                          #4llow                                                                4+                      5 ft/min preheat speed  Low Gloss/Smooth                      180-200° F.     __________________________________________________________________________

EXAMPLES 9 & 10

Coating powders were made as described above from the following components:

    ______________________________________     COMPONENTS                   (A)  (B)      (C)    (D)     ______________________________________     Epoxy Resin GT-7072                     100    --       100  --     Imidazole Adduct P-101                     2.0    --       --   --     2-Phenyl imidazole                     --     --       2.0  --     Flow Aids     MODAFLOW 2000   1.0    1.0      1.0  1.0     (SURFYNOL-104-S)                     1.0    1.0      1.0  1.0     TiO.sub.2 R-902 30     30       30   30     Amine Adduct LMB 5218                     --     100      --   100     Polyethylene (Grade 6A)                     2.0    2.0      2.0  2.0     Sodium hypophosphite                     1.0    1.0      1.0  1.0     Optical brightener                     0.1    0.1      0.1  0.1     ______________________________________

                  TABLE 4     ______________________________________              Component Component Component                                          Component     EXAMPLE  A         B         C       D     ______________________________________      9       65        35        --      --     10       --        --        70      30     ______________________________________

EXAMPLES 11-15

The coating powders of Examples 9 and 10 were deposited on pre-heated wooden panels by tribocharging guns and post-heated on a flat-line conveyor in an oven heated by IR and convection heating according to the conditions given in Table 5 wherein the results are given also.

                                      TABLE 5     __________________________________________________________________________                 Line Speed                       Board Temperature                                Line Speed in                                       Actual Temp.     Mek Rate 50     Ex. #        Powder            Substrate                 of Coating                       Before Coating                                Curing Oven                                       Exiting IR                                               Appearance                                                        Double                                                               Thickness     __________________________________________________________________________     11 Ex. 9            MDF  30 ft/min                       290 (° F.)                                15 ft/min                                       290° F.                                               Good     #4     5 mils     12 Ex. 9            UV-P*                 30 ft/min                       280 (° F.)                                15 ft/min                                       300° F.                                               Very good                                                        #4-5   5 mils     13 Ex. 9            UV-P*                 100 ft/min                       290 (° F.)                                15 ft/min                                       290° F.                                               No pinholes                                                        #4-5   3+     14 Ex. 9            MDF  Hand spray                       280° F.                                 5 ft/min                                       280° F.                                               Very slightly                                                        --llow --                                               Smooth     15  Ex. 10            MDF  20 ft/min                       280° F.                                 5 ft/min                                       285° F.                                               Whiter than Ex.                                                        --     --                                               Slight Microtexture     __________________________________________________________________________      *UV-P stands for particleboard precoated with a UV cured liquid coating

EXAMPLES 16-18

The coating powder of Example 16 is the same as that of example 1 except for the addition of 0.1 part by weight of an optical brightener to both Components A and B. The coating powder of Example 17 is the same as that of Example 16 except for the addition of 1.0 part by weight of IRGAFOS 168 anti-oxidant to both Components A and B of the powder of Example 16. The coating powder of Example 18 is the same as that of Example 16 except for the addition of 1.0 part of IRGANOX 1425 to both Components A and B of the powder of Example 16. A coating powder of Comparative Example 1 is the same as the powder of Example 16 except for the addition of 1.0 part of IRGANOX 1098 to both Components A and B of the powder of Example 16. The powders of Examples 9 and 16-18, as well as the powder of the Comparative Example were deposited by a hand-operated tribocharging gun on to a surface of a 0.5 inch thick wooden panel whose temperature was about 230-250° F. and then cured at 300-310° F. for 30 and 60 seconds. The powders of Examples 1, 9, and 10 were deposited by a hand-operated tribocharging gun on to a surface of a 0.75 inch thick wooden panel whose temperature was about 250-270° F. and then cured at 300-310° F. for 30, 60, and 90 seconds. The SK white color shift of each cured coating, as measured with a MacBeth 2020⁺ spectrophotometer using the CIELAB COLORSPACE Delta B⁺(+) yellowness scale, is given in Table 6.

                  TABLE 6     ______________________________________              Panel  Delta B.sup.*+     EXAMPLE    Thickness                         30 secs.  60 secs.                                         90 secs     ______________________________________      9          0.5 in. 1.7       2.0   --     16         "        3.9       7.9   --     17         "        2.1       3.0   --     18         "        3.4       6.0   --     Comp. Ex.  "        7.7       13.5  --      1         0.75 in. 4.7       9.1   9.5      9         "        2.5       4.2   4.5     10         "        1.5       2.7   2.8     ______________________________________

EXAMPLE 19 COMPONENTS

    ______________________________________                       (A)  (B)     ______________________________________     Epoxy Resin GT-7072 100    --     Imidazole Adduct P-101                         2.0    --     Flow Aid            1.0    1.0     Carbon black        3.0    3.0     Amine Adduct LMB-5218                         --     100     Polyethylene (Grade 6A)                         2.0    2.0     Calcium carbonate   15.0   15.0     Nitrile rubber      17.0   17.0     (NIPOL 1422)     ______________________________________

A cured coating having a tight, fine texture, and a slightly dry feel was obtained when a coating powder, made as described above and having a 70:30 weight ratio of Component A to Component B, was sprayed onto a horizontal panel which had been pre-heated for 5 minutes in a 350° F. oven and then heated for 10 minutes at the same temperature. The cured coating had an MEK rating of 4. When the oven temperatures was 300° F., the MEK rating was the same but the coating felt less dry. 

The subject matter claimed is:
 1. A thermosetting powder coating system in which competing reactions are taking place simultaneously, said reactions being:(A) a catalyzed self-curing of a portion of an epoxy resin present in an extruded mixture of the resin and a catalyst, and (B) a crosslinking reaction between another portion of the extruded resin and a low temperature curing agent;said extruded mixture and said low temperature curing agent both being in powder form and being blended to form a coating powder.
 2. The system of claim 1 wherein the low temperature curing agent of reaction (B) is an epoxy resin adduct of an aliphatic polyamine having a primary amino group.
 3. The system of claim 1 wherein the catalyst of reaction (A) is an epoxy adduct of an imidazole having the general formula: ##STR2## wherein R¹, R², R³, and R⁴ are independently hydrogen or any substituent which is not reactive with the epoxy resin.
 4. The system of claim 1 wherein the reactions occur at a temperature of from about 180° F. up to but not including the decomposition temperature of the blend.
 5. The system of claim 4 wherein the temperature is from about 190° F. to about 290° F.
 6. The system of claim 5 wherein the temperature is from about 190° F. to about 250° F.
 7. The system of claim 4 wherein the epoxy resin is crystalline.
 8. The system of claim 3 wherein R¹, R², R³, and R⁴ are independently alkyl, aryl, alkaryl.
 9. The system of claim 3 wherein R² is methyl, and R¹, R³, and R⁴ are hydrogen.
 10. The system of claim 1 wherein the rate of reactions (A) and (B) are different.
 11. The system of claim 1 wherein the rate of reaction (B) is greater than that of reaction (A).
 12. The system of claim 1 wherein the curing agent is an epoxy adduct of an aliphatic polyamine having a secondary amino group.
 13. A thermosetting powder coating system in which the thermosetting of an extruded mixture of a self-curing epoxy resin and (A) a catalyst or (B) an amount of a low temperature curing agent insufficient to cause substantial curing of the resin during extrusion is facilitated by the separate addition of a low temperature curing agent; said extruded mixture and said separately added low temperature curing agent both being in powder form and being blended to form a coating powder.
 14. The system of claim 13 wherein the low temperature curing agent (B) is a non-catalytic amount of said catalyst which is sufficient to complete the cure.
 15. The system of claim 13 wherein the low temperature curing agent is an epoxy resin adduct of a aliphatic polyamine having a primary amino group.
 16. The system of claim 13 wherein the catalyst is an epoxy adduct of an imidazole having the general formula: ##STR3## wherein R¹, R², R³, and R⁴ are independently hydrogen or any substituent which is not reactive with the epoxy resin.
 17. The system of claim 1 wherein the catalyst of reaction (A) is an imidazole having the general formula: ##STR4## wherein R¹, R², R³, and R⁴ are independently hydrogen or any substituent which is not reactive with the epoxy resin. 